A specialty metal plater in
The rinse water clean up options included reverse osmosis, ion exchange, evaporation, and EC. The reject water from the reverse osmosis concentrated the heavy metals, creating a worse problem for heavy metal water discharge. Ion exchange required continual maintenance of the exchange resin. The maintenance cost to regenerate the resin was estimated to be 50% of the capital cost for the system each year or $0.14 per gallon. The ion exchange capital cost was about the same as the EC capital cost. Evaporation produces a heavy metal ion powder and required about $0.15 per gallon evaporated for energy. The evaporator capital cost was about three times that of the ion exchange or EC capital cost. EC converts the metal ions to an oxide from. The oxides can be separated from the water by settling tanks and filtration. Metal oxides can be disposed of in the regular landfill. The clarified and filtered water is reusable in the metal rinsing process. The EC operating cost is less than $0.01 per gallon.
In September 2001 Joe’s Plating installed a Powell Water Systems, Inc. 3-gpm EC system followed by decant tanks and filtration. The overflow water from the rinse tank is collected in a storage tank. The rinse water is processed through the Powell 3-gpm EC unit, decanted to separate the bulk of the solids, and the clear water is filtered before being recycled to the rinse water tank. The plating shop water use has been reduced from 800 gallons per day to 60 gallons per month, which includes one toilet. The operating cost is about $0.002 per gallon treated.
Joe’s plating has a zero discharge permit. The sludge from the decant tanks is dried in an evaporator and stored in a container for disposal.
This specialty plating shop has eliminated water discharge to the city sewer by utilizing Powell EC to condition the rinse water for reuse.
Step 1. The plated parts are rinsed in a rinse tank. The over flow from the rinse tank flows into an adjacent surge tank as pictured below:
Step 2. The water is pumped from the surge tank into the Powell 3-gpm-EC unit.
Step 3. The water from the Powell EC unit is then pumped into one of two cone bottom tanks. The water is allowed to separate in the tanks. The solids settle to the bottom. The clear water is at the top of the tanks.
Step 4. The clear conditioned water is then pumped back to the rinse tank. The solids are drained off the cone bottom tank periodically and allowed to evaporate in a bucket. The dried solids are then disposed of in the dumpster.
Because there is not discharge to the city sewer from the plating rinse tank, there is no discharge concern.